CN1887765A - Dry cement clinker producing process with carbide residue to replace limy material - Google Patents
Dry cement clinker producing process with carbide residue to replace limy material Download PDFInfo
- Publication number
- CN1887765A CN1887765A CNA2006100910657A CN200610091065A CN1887765A CN 1887765 A CN1887765 A CN 1887765A CN A2006100910657 A CNA2006100910657 A CN A2006100910657A CN 200610091065 A CN200610091065 A CN 200610091065A CN 1887765 A CN1887765 A CN 1887765A
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- CN
- China
- Prior art keywords
- kiln
- cement clinker
- carbide slag
- kiln tail
- dry
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B7/00—Hydraulic cements
- C04B7/14—Cements containing slag
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The present invention relates to building material technology, and is especially dry cement clinker producing process with carbide residue to replace limy material completely. The dry cement clinker producing process includes the following steps: compounding sandstone, fly ash, sulfuric acid slag and water and wet grinding to obtain slurry; concentrating carbide residue in a thickener; mixing the slurry with concentrated carbide residue through stirring with compressed air to form raw material slurry; pumping the raw material slurry to press filter for extruding to dewater to form material cake; stoving, crushing and heat exchanging with fume from rotary kiln to form material powder; and calcining at 1250-1350 deg.c in rotary kiln to produce cement clinker. The present invention makes it possible to eliminate pollution caused by carbide residue completely.
Description
1, technical field: carbide slag 100% of the present invention substitutes natural calcareous raw material dry cement clinker producing processing method and relates to building materials field, relates in particular to a kind of production technique of carbide slag cement grog.
2, background technology: the industrial residue that some chemical plant are produced in producing is more, as carbide slag, sulfate slag, flyash etc., directly abandons these waste residues and be the significant wastage to resource, can pollute ecotope again.These industrial residues can be used as resource reutilization fully, especially are rich in CaO in the carbide slag, can be used as the surrogate of Wingdale raw material in the manufacture of cement.Application number be the patent of invention " is the cement clinker and the dry method production process thereof of raw material with carbide slag " of CN200510021024.6 to disclose a kind of be main raw material with the carbide slag, adopt the dry method shaft kiln to prepare the method for cement clinker.Its proportioning raw materials is: carbide slag 60～70%, phosphorus slag 3～8%, pyrite cinder 1～3%, phosphogypsum 1～4%, flyash 8～17%, hard coal 8～10%, adopt planetary wheel roller to stir and reach stone roller, extrusion homogenizing, extruding, dehydration, balling-up, integrated dry method is made grog.This method has the following disadvantages:
1. the carbide slag addition content is few, only reaches 60～70%; 2. level of automation is low, owing to adopt the dry method shaft kiln calcination, so need manual operation, labour intensity is big; 3. clinker quality instability; 4. small scale because the shaft kiln scale only is 7～80,000 tons/single line of annual output, can not satisfy the needs of scale operation.
3, summary of the invention: the object of the present invention is to provide a kind ofly to replace natural calcareous raw material fully the method that adopts the calcining of wet-milling and dry-process rotory kiln to produce cement clinker with carbide slag.
The objective of the invention is to be achieved by the following technical programs:
Raw materials used and weight (kg) is when preparing 1 ton of cement clinker:
Carbide slag: 700-850kg sandstone: 50-150kg flyash: 70-170kg
Sulfate slag: 10-50kg water: 500-630kg.
Processing method:
1. earlier sandstone, flyash and three kinds of auxiliary materials of sulfate slag are ground by charging feed behind the above-mentioned weight batching, add water simultaneously and carry out wet-milling, it is standby that the slip behind the mill pumps into the auxiliary material pulp stock;
2. with carbide slag after thickener concentrates, make its moisture content reduce to 70% by 90%, it is standby to send into the carbide slag slurries storehouse;
3. auxiliary material slip and carbide slag slurries are sent into pulp stock respectively and be made into slip, stir by the storehouse compressed air, subsequently the charge pulp that stirs is pumped into the plate and frame(type)filter press extrusion dehydration, make its moisture≤37%, form raw material material cake, this material cake is through rubber conveyer, rotary feeder feeding oven dry hammer mill;
4. the material cake at oven dry hammer mill material feeding box contacts with the 550-750 ℃ of hot flue gas of introducing from dry-process rotory kiln kiln tail smoke-box, carry out the intensive heat exchange, entering crusher chamber together with hot gas flow is subsequently broken up, and continuation and kiln tail waste heat carry out sufficient heat exchange, tiny powdered material after oven dry is broken up is the raw material finished product, its water content≤1-4%, be brought into increase in pipeline with hot blast and enter the cyclone collection, send into kiln tail current stabilization feed trap subsequently, again through the duplex tube helix feeding machine, tremie pipe enters in the dry-process rotory kiln, and calcining 30-40 minute down at 1250 ℃-1350 ℃ is ripe material.For the thick cooking starch of not oven dry of water content 〉=4%, continue in crusher chamber, to dry to break up, collect until being brought into cyclone by hot flue gas.
5. the dust-laden exhaust gas that goes out cyclone enters kiln tail dust precipitator, purifies after kiln tail exhaust blower, chimney enter atmosphere.The kiln ash that kiln tail smoke-box and dust precipitator are collected is sent into the kiln tail again by chain conveyor, board chain hoisting machine and is gone back to grey storehouse, and the kiln ash in grey storehouse is in rubber conveyer is sent into kiln tail current stabilization feed trap feeding kiln.
The present invention adopts carbide slag 100% to substitute natural calcareous wet-milling dry method calcining process, raw material material cake to water content after the press filtration≤37%, adopt the high oven dry hammer mill of thermo-efficiency to dry and fragmentation, the oven dry thermal source all utilizes kiln tail waste heat flue gas, dry outside kiln, raw material dry powder is calcined directly into dry-process rotory kiln.Adopt this processing method to handle 27.6 tons of chemical plant carbide slags, 0.7 ton of sulfate slag, 80,000 tons in flyash has solved industrial residue fully to the social concern that ecotope pollutes, and has realized the utilization again of resource.
This processing method makes and effectively reduce production costs industrial residue comprehensive utilization ratio height in the protection environment.Kiln unit volume output height, single kiln throughput is big, and power consumption is few, and cement quality is stable.
4, embodiment:
Embodiment: raw materials used and weight (kg) is when preparing 1 ton of cement clinker:
Carbide slag: 700-850kg sandstone: 50-150kg flyash: 70-170kg
Sulfate slag: 10-50kg water: 500-630kg.
Processing method: 1. earlier with sandstone, flyash and three kinds of auxiliary materials of sulfate slag by behind the above-mentioned weight batching again in rubber conveyer feeding Φ 2 * 11m G=18t/h raw mill, add entry 500-630kg simultaneously and carry out wet grinding, auxiliary material slip behind the grinding draws off from the mill tail, slurry vessel through tilting flows in the slip hole, and it is standby to send into the auxiliary material pulp stock by the slag stock pump again.
2. with carbide slag after Φ 20m thickener concentrates, make its moisture content reduce to 70% by 90%, it is standby to send into the carbide slag slurries storehouse through the slag stock pump.
3. auxiliary material slip and carbide slag slurries are sent into pulp stock respectively through the slag stock pump and be made into qualified slip.By air compressor machine pressurized air is sent into from the slip bottom of the reservior and to be stirred, to prevent the slip precipitation.With after 80NG80 slag stock pump pumps into XMZ-600/1600 template frame pressure filter extruding with the charge pulp that stirs, make its moisture≤37%, form the raw material filter cake, this filter cake is transported to rubber conveyer earlier by the XGZ-800 scraper plate machine under the pressure filter, be transported to Φ 1200mm rotary feeder again, enter subsequently in the PCG-2821 oven dry hammer mill and pulverize, introducing 550-750 ℃ of hot flue gas from Φ 4.3 * 96m G=1000t/d rotary kiln smoke-box when pulverizing dries, Powdered finished product after the oven dry is raw material, its water content≤1-4%.
4. the material cake at oven dry hammer mill material feeding box contacts with the 550-750 ℃ of hot flue gas of introducing from the rotary kiln smoke-box, carry out the intensive heat exchange, entering crusher chamber together with hot gas flow is subsequently broken up, and continuation and kiln tail waste heat carry out sufficient heat exchange, tiny powdered material after oven dry is broken up is the raw material finished product, its water content≤1-4%, being brought into increase in pipeline with hot flue gas enters 4-Φ 3.2m cyclone and is collected, send into kiln tail current stabilization feed trap subsequently, again through LE350 * 3500mm duplex tube helix feeding machine, tremie pipe enters in the rotary kiln, and calcining 30-40 minute down at 1250 ℃-1350 ℃ is ripe material.For the thick cooking starch of not oven dry of water content 〉=4%, continue in crusher chamber, to dry to break up, when water content was 1-4%, its deadweight lightened, and can be brought into cyclone by hot flue gas and collect.
5. go out about 180 ℃ of the dust-laden exhaust gas temperature of cyclone, it enters kiln tail dust precipitator, purifies after kiln tail exhaust blower, chimney enter atmosphere.The kiln ash that kiln tail smoke-box and dust precipitator are collected is sent into the kiln tail again by chain conveyor, board chain hoisting machine and is gone back to grey storehouse, and the kiln ash in grey storehouse is in rubber conveyer is sent into kiln tail current stabilization feed trap feeding kiln.
Claims (2)
1, a kind of carbide slag 100% substitutes the cement clinker of natural calcareous raw material dry production, it is characterized in that:
Raw materials used and weight (kg) is when preparing 1 ton of cement clinker:
Carbide slag: 700-850kg sandstone: 50-150kg flyash: 70-170kg
Sulfate slag: 10-50kg water: 500-630kg.
2, a kind of carbide slag 100% substitutes the cement clinker of natural calcareous raw material dry production, it is characterized in that:
Processing method is:
1. earlier sandstone, flyash and three kinds of auxiliary materials of sulfate slag are ground by charging feed behind the described weight batching of claim 1, add water simultaneously and carry out wet-milling, it is standby that the slip behind the mill pumps into the auxiliary material pulp stock;
2. with carbide slag after thickener concentrates, make its moisture content reduce to 70% by 90%, it is standby to send into the carbide slag slurries storehouse;
3. auxiliary material slip and carbide slag slurries are sent into pulp stock respectively and be made into slip, stir by the storehouse compressed air, subsequently the charge pulp that stirs is pumped into the plate and frame(type)filter press extrusion dehydration, make its moisture≤37%, form raw material material cake, this material cake is through rubber conveyer, rotary feeder feeding oven dry hammer mill;
4. the material cake at oven dry hammer mill material feeding box contacts with the 550-750 ℃ of hot flue gas of introducing from the rotary kiln smoke-box, carry out the intensive heat exchange, entering crusher chamber together with hot gas flow is then broken up, and continuation and kiln tail waste heat carry out sufficient heat exchange, its water content≤1-4% of tiny powdered material after oven dry is broken up, be brought into increase in pipeline with hot flue gas and enter the cyclone collection, send into kiln tail current stabilization feed trap subsequently, enter in the rotary kiln through duplex tube helix feeding machine, tremie pipe, calcining 30-40 minute down at 1250 ℃-1350 ℃ is ripe material again; For the thick cooking starch of not oven dry of water content 〉=4%, continue in crusher chamber, to dry to break up, collect until being brought into cyclone by hot flue gas;
5. the dust-laden exhaust gas that goes out cyclone enters kiln tail dust precipitator, purify after kiln tail exhaust blower, chimney enter atmosphere, the kiln ash that kiln tail smoke-box and dust precipitator are collected, send into the kiln tail again by chain conveyor, board chain hoisting machine and go back to grey storehouse, the kiln ash in grey storehouse is in rubber conveyer is sent into kiln tail current stabilization feed trap feeding kiln.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100910657A CN100453489C (en) | 2006-07-13 | 2006-07-13 | Dry cement clinker producing process with carbide residue to replace limy material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100910657A CN100453489C (en) | 2006-07-13 | 2006-07-13 | Dry cement clinker producing process with carbide residue to replace limy material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1887765A true CN1887765A (en) | 2007-01-03 |
| CN100453489C CN100453489C (en) | 2009-01-21 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNB2006100910657A Expired - Fee Related CN100453489C (en) | 2006-07-13 | 2006-07-13 | Dry cement clinker producing process with carbide residue to replace limy material |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103466977A (en) * | 2013-09-03 | 2013-12-25 | 北京工业大学 | Method for preparing substitutive raw material of cement |
| CN103813989A (en) * | 2011-10-19 | 2014-05-21 | 电气化学工业株式会社 | Process for dewatering slurry |
| CN105541141A (en) * | 2015-12-23 | 2016-05-04 | 天能水泥有限公司 | A device and a method for preparing cement from dry and wet calcium carbide slag |
| CN106186748A (en) * | 2016-08-26 | 2016-12-07 | 安徽皖维高新材料股份有限公司 | The recycling system of a kind of industrial waste carbide slag and recoverying and utilizing method |
| CN107200486A (en) * | 2017-07-11 | 2017-09-26 | 陕西北元化工集团股份有限公司 | A kind of highly doped industrial residue cement and preparation method thereof |
| CN115212713A (en) * | 2022-05-30 | 2022-10-21 | 湖北工业大学 | Carbon sequestration and emission reduction method for wet grinding kiln ash of cement plant |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1296305C (en) * | 2005-06-03 | 2007-01-24 | 郑维平 | Cement clinker using carbide slag as raw material and drying production process thereby |
-
2006
- 2006-07-13 CN CNB2006100910657A patent/CN100453489C/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103813989A (en) * | 2011-10-19 | 2014-05-21 | 电气化学工业株式会社 | Process for dewatering slurry |
| CN103813989B (en) * | 2011-10-19 | 2016-01-20 | 电化株式会社 | The dewatering of mud |
| CN103466977A (en) * | 2013-09-03 | 2013-12-25 | 北京工业大学 | Method for preparing substitutive raw material of cement |
| CN105541141A (en) * | 2015-12-23 | 2016-05-04 | 天能水泥有限公司 | A device and a method for preparing cement from dry and wet calcium carbide slag |
| CN106186748A (en) * | 2016-08-26 | 2016-12-07 | 安徽皖维高新材料股份有限公司 | The recycling system of a kind of industrial waste carbide slag and recoverying and utilizing method |
| CN106186748B (en) * | 2016-08-26 | 2018-07-27 | 安徽皖维高新材料股份有限公司 | A kind of recycling system and recoverying and utilizing method of industrial waste carbide slag |
| CN107200486A (en) * | 2017-07-11 | 2017-09-26 | 陕西北元化工集团股份有限公司 | A kind of highly doped industrial residue cement and preparation method thereof |
| CN115212713A (en) * | 2022-05-30 | 2022-10-21 | 湖北工业大学 | Carbon sequestration and emission reduction method for wet grinding kiln ash of cement plant |
| CN115212713B (en) * | 2022-05-30 | 2024-03-26 | 湖北工业大学 | Method for carbon fixation and emission reduction of wet mill kiln ash of cement plant |
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| Publication number | Publication date |
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| CN100453489C (en) | 2009-01-21 |
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Legal Events
| Date | Code | Title | Description |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20061215 Address after: No. 12 West Rainbow Road, the Xinjiang Uygur Autonomous Region, Urumqi Applicant after: Xinjiang Construction Material Design & Research Institute Co.,Ltd. Address before: No. 1 West Rainbow Road, the Xinjiang Uygur Autonomous Region, Urumqi Applicant before: Xinjiang Construction Material Design & Research Institute Co.,Ltd. Co-applicant before: Shihezi Development Zone Qingsong Tianye Cement Co.,Ltd. |
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| C14 | Grant of patent or utility model | ||
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| ASS | Succession or assignment of patent right |
Owner name: XINJIANG TRIUMPH BUILDING MATERIALS DESIGNING INST Free format text: FORMER OWNER: XINJIANG BUILDING MATERIAL DESIGN INST., (CO., LTD.) Effective date: 20101027 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20101027 Address after: 830000 No. 12 West Rainbow Road, the Xinjiang Uygur Autonomous Region, Urumqi Patentee after: Xinjiang Triumph Building Materials Designing Institute Co.,Ltd. Address before: 830000 No. 12 West Rainbow Road, the Xinjiang Uygur Autonomous Region, Urumqi Patentee before: Xinjiang Construction Material Design & Research Institute Co.,Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090121 |
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| CF01 | Termination of patent right due to non-payment of annual fee |